EPRI’s Low CO2 Emission
                                                                      Coal Power Research,
                                                                      Development and
                                                                      Demonstration Programs



                                                                                   November 2009

                                                                                 Jeffrey N. Phillips
                                                                                Sr. Program Manager
                                                                             Advanced Generation Options


© 2009 Electric Power Research Institute, Inc. All rights reserved.      1
Introduction

     • EPRI’s efforts are focused on:
        – Reducing CO2 emissions on kg/MWhr basis by
          increasing thermal efficiency of coal power plants
        – Improving the economics of pre-combustion, post-
          combustion, and oxy-combustion CO2 capture
          technologies
     • EPRI’s efforts range from lab tests to large
       demonstrations




© 2009 Electric Power Research Institute, Inc. All rights reserved.   2
Decreasing CO2 Emissions with More Efficient
                               Designs




© 2009 Electric Power Research Institute, Inc. All rights reserved.   3
Increased Efficiency = Reduced Fuel & Emissions




                                                                                 Advanced steam
                                                                                 conditions can reduce
                                                                                 CO2 emissions by 30-33%
                                                                                 compared to average U.S.
                                                                                 coal power plant




                  Adapted by I.Wright, ORNL from B. Vitalis, Babcock Power


© 2009 Electric Power Research Institute, Inc. All rights reserved.          4
Advanced-Ultrasupercritical Steam Boiler
   Consortium Phase I & II
                         1: Conceptual
                         Design
                         2: Material Properties
                         3: Steamside
                         Oxidation
                         4: Fireside Corrosion                   8: Design Data & Rules
                                                                    (including Code
                         5: Welding                              interface)
                         6:
                         Fabricability


                    7:
                    Coatings




      Develop the materials technology to fabricate
                and operate a A-USC Steam Boiler with
                         Steam Parameter up to 760°C
                                                                5
© 2009 Electric Power Research Institute, Inc. All rights reserved.
Advanced-Ultrasupercritical Steam Turbine
     Consortium Phase II

• Steam Conditions from boiler and phase I turbine studies
      – 730°C, 39MPa Main Steam
      – 760°C, Re-heat
      – Size to 1000MW
• Tasks
      – Rotor/Disc Testing (near full-size forgings)
      – Blade/Airfoil Alloy Testing
      – Valve Internals Alloy Testing
      – Rotor Alloy Welding and Characterization
      – Cast Casing Alloy Testing
      – Casing Welding and Repair
© 2009 Electric Power Research Institute, Inc. All rights reserved.   6
Economic Analysis Shows Advanced USC
     Provides Cost-Effective CO2 Reductions

                                                                          582ºC      680ºC
                                                                          SCPC        A-USC
     Thermal Efficiency, %HHV                                              38.5        42.7

     Levelized Cost of Electricity $/                                     53.3          55.3
     MWh
     CO2 emissions, kg/MWh                                                853            765

     Avoided CO2 emissions cost,                                          N/A           22.5
     $/metric ton vs. 582ºC SCPC

                                  Reference: EPRI Technical Report 1015699, September 2008

© 2009 Electric Power Research Institute, Inc. All rights reserved.   7
CoalFleet IGCC User Design Basis
     Specification (see EPRI Report 1017501, Nov. 2009)

     • Defines power company technical requirements for a site-
       specific IGCC plant; supplier alliances to propose plants
       that meet the UDBS                                        EPR I
     • UDBS represents major collaborative effort
                                                                                                             TION
                                                                                                    CIFICA
                                                                                             IS SPE
             – All sectors of industry engaged                            US E R
                                                                                 DESIG
                                                                                       N BAS
                                                                                             101750
                                                                                                    1
                                                                                      Report

             – 30+ people developed UDBS Ver. 9
             – Approved by all CoalFleet members
     • Robust, 1600-page industry-developed
       and tested guideline, primer, and
       lessons-learned compendium
     • Flexible, yet promoting of standardized, optimized designs
     • Already in use by numerous CoalFleet participants

© 2009 Electric Power Research Institute, Inc. All rights reserved.   8
IGCC Case Studies
     Performance Summary (see EPRI Report 1019368, October 2009)




© 2009 Electric Power Research Institute, Inc. All rights reserved.   9
IGCC Engineering and Economic Evaluations
     2009–10 Study Content


• 50 Hz F-Frame Gas Turbine Cases
        – Northeast Netherlands site
• Coal Type
        – Eastern Australian export coal
• Gasification Technologies
        – General Electric, Siemens, Shell,
          Prenflo PDQ, Mitsubishi Heavy Industries, ConocoPhillips
• Greenfield Carbon Capture and Storage
• Sensitivity Analyses
        – G-Frame GT, Cost Estimates for CO2 Liquefaction and HP
          Gasification cases
• 2008–09 Capital Costs Revisited


© 2009 Electric Power Research Institute, Inc. All rights reserved.   10
ITM for Low Cost Oxygen Production
     Overview


     • A ceramic membrane to separate oxygen from air
     • Intermediate-sized 150 tons O2/day test unit integrated with 5-15 MWe
       turbomachinery system
             – Utilizes commercial-scale ceramic membrane modules for
               oxygen separation
             – Representative of arrangement for full-scale
               IGCC plant with CCS
                                                                           0.5 tons O2/day ITM
     • Three-year program to design,
       build, and test system                                                   Modules
             – Team: Air Products (with Ceramatec and
               Siemens), DOE, and EPRI
     • EPRI has launched the collaborative
             – Builds on major investments by Air Products and DOE
             – Will incorporate real-world utility plant design and
               integration considerations
             – Forms a bridge to commercial IGCC application                             Images courtesy Air Products.

             – May enhance oxy-combustion applications                               © Air Products. All rights reserved.




     • Additional organizations are welcome to join the collaborative

© 2009 Electric Power Research Institute, Inc. All rights reserved.   11
ITM for Low Cost Oxygen Production
     Potential Benefits


     • Reduces barriers to IGCC technology
       deployment
             – Decreases capital cost by ~7%
             – Decreases auxiliary power consumption by ~6%
             – Improves plant efficiency by ~1 percentage point
             – Reduces oxygen plant footprint by 50%
             – Reduces cooling water requirement by 60%
     • Large forecast growth in oxygen plant market should drive
       learning-by-doing cost reduction after commercialization
     • Potential use with oxy-combustion boilers




© 2009 Electric Power Research Institute, Inc. All rights reserved.   12
Improving the Economics of CO2 Capture &
                                      Storage




© 2009 Electric Power Research Institute, Inc. All rights reserved.   13
Challenges for Post-Combustion CO2 Capture

     • What to do with CO2?
             – SO2: ~                     1,400 ppmv in flue gas            Can’t use consumable sorbents for CO2
                                                                           capture (like those used for SO2 Capture).
             – CO2: ~140,000 ppmv in flue gas
     • Concentrating flue gas CO2
             – Best option at present: scrub the gas with highly alkaline solutions which can then be
               stripped of the CO2
     • Putting the CO2 in the ground (required pressures: 100 – 175 bar)
     • The overall capacity/efficiency penalty with current technology:
             – 750 MW plant will net 492 MW with CO2 Capture (258 MW loss)




© 2009 Electric Power Research Institute, Inc. All rights reserved.   14
Capture Technologies Reviewed
     (see EPRI Report 1016995)

    Absorption, Liquid                                                Absorption, Liquid, cont.          Membrane, Active
    •    MHI, KS-1                                                    •InnoSepra                         •   MTR
    •    Chilled Ammonia (CAP)                                        •CarbonTrap                        •   RITE, Cardo polyimide
    •    CANSOLV                                                      •TNO CASTOR2                       •   Tetramer Technologies
    •    "7/2" MEA & PZ                                               •JustCatch                         •   Poly(Ionic Liquid) Membrane
    •    CASTOR Solvent                                               •CO2 Solution                      •   NanoGloWa
    •    IFP, Dual Phase                                              •Three H Technologies, Inc.        Membrane, Support
    •    Econamine FG+                                                •Catalyte                          •   Carbozyme
    •    PowerSpan ECO2                                               Absorption, Solid                  •   Coral
    •    Ionic Liquids, Notre Dame                                    •RTI                               •   Kvaerner Membrane Contactor
    •    Sargas                                                       •Hyperbranched Polyamine           •   PureStream
    •    Skyonic Skymine                                              •Polyethyleneimine (PEI)           Cryogenic
    •    AWL                                                          •Amine on inert support            • CO2 Frosting
    •    WowClean                                                     •CO2 Wheel, Toshiba                • Enecogen
    •    Ionic Liquids, U. S. Carolina
                                                                      Adsorption                         Biological Fixation
    •    MEA:MDEA                                                     •Metal Organic Frameworks (MOFs)   •
    •    COCS Solvent, RITE                                                                                  UNLV PRB
                                                                      •Advanced Mesoporous Materials     •
    •    GRT                                                                                                 Independence BioProducts
                                                                      •Heavy Reflux PSA                  •
    •    Immobilized Activator                                                                               Carbon Capture Corp.
                                                                      •CO2CRC Adsorbent                  •
    •    Enzyme Catalysis                                                                                    GreenFuel
                                                                      •U. Akron                          •
    •    AEEA                                                                                                GSCleanTech
                                                                      •U. Wyoming carbonaceous sorbent   •
    •    D3                                                                                                  Conc. Solar Photoreactor
                                                                      •ADA-ES                            •
    •    HTC Purenergy                                                                                       Many new Algae Systems
                                                                      •VMI
    •    RCO2
© 2009 Electric Power Research Institute, Inc. All rights reserved.   Mineralization    15
Assessing Technical Readiness Level (TRL)

      TRL-9 Full-Scale Commercial                                          • Most candidate CO2 removal
            Deployment                                                       technologies assessed are
                                                                             still a “twinkle in the eye”
      TRL-8 Sub-Scale Commercial
            Demonstration Plant                                            • Significant development time
                                                                             required to bring even the
      TRL-7 Pilot Plant, 5 to 25% of full-scale
                                                                             most ready technology to
      TRL-6 Process Development Unit <5%                                     TRL-9
      TRL-5 Component Test in Relevant




                                                                             # Technologies at indicated TRL
            Environment
      TRL-4 Laboratory Component Testing
      TRL-3 Analytical, “Proof of Concept”
      TRL-2 Application Formulated
      TRL-1 Basic Principles Observed

© 2009 Electric Power Research Institute, Inc. All rights reserved.   16
AEP-Alstom Chilled Ammonia Post-Combustion
     CO2 Capture Scale-Up – Overview
    • ~20 MWe demonstration facility
      at AEP’s Mountaineer plant
             • ~90,000 tonnes-CO2/yr
             – Next development step after 1.7 MWe
               R&D pilot at We Energies’ Pleasant
               Prairie Power Plant
             – Injection into two on-site wells
                                                                           PVF 2-23-09, Photo courtesy of AEP/Alstom. All rights reserved.
             – 1–5 year injection program plus
               post-injection monitoring
             – Started capturing CO2 on September 1 and injecting on October 1
    • Alstom designed and built the facility, and will serve as lead operator for
      the first year. AEP may operate the facility for an additional 1-4 years.
    • EPRI will measure and report unit performance, operability, and reliability
      over project duration; EPRI will also monitor CO2 storage performance

© 2009 Electric Power Research Institute, Inc. All rights reserved.   17
Southern Co.-MHI KM-CDR Advanced Amine
     Post-Combustion CO2 Capture – Overview
    • ~25 MWe demonstration facility at Alabama Power’s Plant Barry
      (~ 140,000 tonnes-CO2/year)
             – Potentially lower regeneration energy than other amines; less corrosive;
               low O2 degradation
             – Injection program under U.S. DOE’s Southeast Regional Carbon
               Sequestration Partnership (SECARB) Project—ongoing
             – 4 years of CO2 injection plus 4 years of post-injection monitoring
             – Startup scheduled for 4th Quarter 2010
    • Southern Co. is leading the project and will install and operate the
      plant; MHI is designing the CO2 capture facility
    • EPRI will measure and report CO2 capture performance, operability,
      and reliability
    • EPRI is managing CO2 injection and monitoring operations under U.S.
      DOE research partnership
© 2009 Electric Power Research Institute, Inc. All rights reserved.   18
Questions?




                     Together…Shaping the Future of Electricity

                                                                        Jeffrey Phillips
                                                                      jphillip@epri.com
                                                                           Jong Kim
                                                                       jkim@epri.com




© 2009 Electric Power Research Institute, Inc. All rights reserved.           19

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EPRI Low CO2 Emission Coal R&amp;D For Kpic

  • 1. EPRI’s Low CO2 Emission Coal Power Research, Development and Demonstration Programs November 2009 Jeffrey N. Phillips Sr. Program Manager Advanced Generation Options © 2009 Electric Power Research Institute, Inc. All rights reserved. 1
  • 2. Introduction • EPRI’s efforts are focused on: – Reducing CO2 emissions on kg/MWhr basis by increasing thermal efficiency of coal power plants – Improving the economics of pre-combustion, post- combustion, and oxy-combustion CO2 capture technologies • EPRI’s efforts range from lab tests to large demonstrations © 2009 Electric Power Research Institute, Inc. All rights reserved. 2
  • 3. Decreasing CO2 Emissions with More Efficient Designs © 2009 Electric Power Research Institute, Inc. All rights reserved. 3
  • 4. Increased Efficiency = Reduced Fuel & Emissions Advanced steam conditions can reduce CO2 emissions by 30-33% compared to average U.S. coal power plant Adapted by I.Wright, ORNL from B. Vitalis, Babcock Power © 2009 Electric Power Research Institute, Inc. All rights reserved. 4
  • 5. Advanced-Ultrasupercritical Steam Boiler Consortium Phase I & II 1: Conceptual Design 2: Material Properties 3: Steamside Oxidation 4: Fireside Corrosion 8: Design Data & Rules (including Code 5: Welding interface) 6: Fabricability 7: Coatings Develop the materials technology to fabricate and operate a A-USC Steam Boiler with Steam Parameter up to 760°C 5 © 2009 Electric Power Research Institute, Inc. All rights reserved.
  • 6. Advanced-Ultrasupercritical Steam Turbine Consortium Phase II • Steam Conditions from boiler and phase I turbine studies – 730°C, 39MPa Main Steam – 760°C, Re-heat – Size to 1000MW • Tasks – Rotor/Disc Testing (near full-size forgings) – Blade/Airfoil Alloy Testing – Valve Internals Alloy Testing – Rotor Alloy Welding and Characterization – Cast Casing Alloy Testing – Casing Welding and Repair © 2009 Electric Power Research Institute, Inc. All rights reserved. 6
  • 7. Economic Analysis Shows Advanced USC Provides Cost-Effective CO2 Reductions 582ºC 680ºC SCPC A-USC Thermal Efficiency, %HHV 38.5 42.7 Levelized Cost of Electricity $/ 53.3 55.3 MWh CO2 emissions, kg/MWh 853 765 Avoided CO2 emissions cost, N/A 22.5 $/metric ton vs. 582ºC SCPC Reference: EPRI Technical Report 1015699, September 2008 © 2009 Electric Power Research Institute, Inc. All rights reserved. 7
  • 8. CoalFleet IGCC User Design Basis Specification (see EPRI Report 1017501, Nov. 2009) • Defines power company technical requirements for a site- specific IGCC plant; supplier alliances to propose plants that meet the UDBS EPR I • UDBS represents major collaborative effort TION CIFICA IS SPE – All sectors of industry engaged US E R DESIG N BAS 101750 1 Report – 30+ people developed UDBS Ver. 9 – Approved by all CoalFleet members • Robust, 1600-page industry-developed and tested guideline, primer, and lessons-learned compendium • Flexible, yet promoting of standardized, optimized designs • Already in use by numerous CoalFleet participants © 2009 Electric Power Research Institute, Inc. All rights reserved. 8
  • 9. IGCC Case Studies Performance Summary (see EPRI Report 1019368, October 2009) © 2009 Electric Power Research Institute, Inc. All rights reserved. 9
  • 10. IGCC Engineering and Economic Evaluations 2009–10 Study Content • 50 Hz F-Frame Gas Turbine Cases – Northeast Netherlands site • Coal Type – Eastern Australian export coal • Gasification Technologies – General Electric, Siemens, Shell, Prenflo PDQ, Mitsubishi Heavy Industries, ConocoPhillips • Greenfield Carbon Capture and Storage • Sensitivity Analyses – G-Frame GT, Cost Estimates for CO2 Liquefaction and HP Gasification cases • 2008–09 Capital Costs Revisited © 2009 Electric Power Research Institute, Inc. All rights reserved. 10
  • 11. ITM for Low Cost Oxygen Production Overview • A ceramic membrane to separate oxygen from air • Intermediate-sized 150 tons O2/day test unit integrated with 5-15 MWe turbomachinery system – Utilizes commercial-scale ceramic membrane modules for oxygen separation – Representative of arrangement for full-scale IGCC plant with CCS 0.5 tons O2/day ITM • Three-year program to design, build, and test system Modules – Team: Air Products (with Ceramatec and Siemens), DOE, and EPRI • EPRI has launched the collaborative – Builds on major investments by Air Products and DOE – Will incorporate real-world utility plant design and integration considerations – Forms a bridge to commercial IGCC application Images courtesy Air Products. – May enhance oxy-combustion applications © Air Products. All rights reserved. • Additional organizations are welcome to join the collaborative © 2009 Electric Power Research Institute, Inc. All rights reserved. 11
  • 12. ITM for Low Cost Oxygen Production Potential Benefits • Reduces barriers to IGCC technology deployment – Decreases capital cost by ~7% – Decreases auxiliary power consumption by ~6% – Improves plant efficiency by ~1 percentage point – Reduces oxygen plant footprint by 50% – Reduces cooling water requirement by 60% • Large forecast growth in oxygen plant market should drive learning-by-doing cost reduction after commercialization • Potential use with oxy-combustion boilers © 2009 Electric Power Research Institute, Inc. All rights reserved. 12
  • 13. Improving the Economics of CO2 Capture & Storage © 2009 Electric Power Research Institute, Inc. All rights reserved. 13
  • 14. Challenges for Post-Combustion CO2 Capture • What to do with CO2? – SO2: ~ 1,400 ppmv in flue gas Can’t use consumable sorbents for CO2 capture (like those used for SO2 Capture). – CO2: ~140,000 ppmv in flue gas • Concentrating flue gas CO2 – Best option at present: scrub the gas with highly alkaline solutions which can then be stripped of the CO2 • Putting the CO2 in the ground (required pressures: 100 – 175 bar) • The overall capacity/efficiency penalty with current technology: – 750 MW plant will net 492 MW with CO2 Capture (258 MW loss) © 2009 Electric Power Research Institute, Inc. All rights reserved. 14
  • 15. Capture Technologies Reviewed (see EPRI Report 1016995) Absorption, Liquid Absorption, Liquid, cont. Membrane, Active • MHI, KS-1 •InnoSepra • MTR • Chilled Ammonia (CAP) •CarbonTrap • RITE, Cardo polyimide • CANSOLV •TNO CASTOR2 • Tetramer Technologies • "7/2" MEA & PZ •JustCatch • Poly(Ionic Liquid) Membrane • CASTOR Solvent •CO2 Solution • NanoGloWa • IFP, Dual Phase •Three H Technologies, Inc. Membrane, Support • Econamine FG+ •Catalyte • Carbozyme • PowerSpan ECO2 Absorption, Solid • Coral • Ionic Liquids, Notre Dame •RTI • Kvaerner Membrane Contactor • Sargas •Hyperbranched Polyamine • PureStream • Skyonic Skymine •Polyethyleneimine (PEI) Cryogenic • AWL •Amine on inert support • CO2 Frosting • WowClean •CO2 Wheel, Toshiba • Enecogen • Ionic Liquids, U. S. Carolina Adsorption Biological Fixation • MEA:MDEA •Metal Organic Frameworks (MOFs) • • COCS Solvent, RITE UNLV PRB •Advanced Mesoporous Materials • • GRT Independence BioProducts •Heavy Reflux PSA • • Immobilized Activator Carbon Capture Corp. •CO2CRC Adsorbent • • Enzyme Catalysis GreenFuel •U. Akron • • AEEA GSCleanTech •U. Wyoming carbonaceous sorbent • • D3 Conc. Solar Photoreactor •ADA-ES • • HTC Purenergy Many new Algae Systems •VMI • RCO2 © 2009 Electric Power Research Institute, Inc. All rights reserved. Mineralization 15
  • 16. Assessing Technical Readiness Level (TRL) TRL-9 Full-Scale Commercial • Most candidate CO2 removal Deployment technologies assessed are still a “twinkle in the eye” TRL-8 Sub-Scale Commercial Demonstration Plant • Significant development time required to bring even the TRL-7 Pilot Plant, 5 to 25% of full-scale most ready technology to TRL-6 Process Development Unit <5% TRL-9 TRL-5 Component Test in Relevant # Technologies at indicated TRL Environment TRL-4 Laboratory Component Testing TRL-3 Analytical, “Proof of Concept” TRL-2 Application Formulated TRL-1 Basic Principles Observed © 2009 Electric Power Research Institute, Inc. All rights reserved. 16
  • 17. AEP-Alstom Chilled Ammonia Post-Combustion CO2 Capture Scale-Up – Overview • ~20 MWe demonstration facility at AEP’s Mountaineer plant • ~90,000 tonnes-CO2/yr – Next development step after 1.7 MWe R&D pilot at We Energies’ Pleasant Prairie Power Plant – Injection into two on-site wells PVF 2-23-09, Photo courtesy of AEP/Alstom. All rights reserved. – 1–5 year injection program plus post-injection monitoring – Started capturing CO2 on September 1 and injecting on October 1 • Alstom designed and built the facility, and will serve as lead operator for the first year. AEP may operate the facility for an additional 1-4 years. • EPRI will measure and report unit performance, operability, and reliability over project duration; EPRI will also monitor CO2 storage performance © 2009 Electric Power Research Institute, Inc. All rights reserved. 17
  • 18. Southern Co.-MHI KM-CDR Advanced Amine Post-Combustion CO2 Capture – Overview • ~25 MWe demonstration facility at Alabama Power’s Plant Barry (~ 140,000 tonnes-CO2/year) – Potentially lower regeneration energy than other amines; less corrosive; low O2 degradation – Injection program under U.S. DOE’s Southeast Regional Carbon Sequestration Partnership (SECARB) Project—ongoing – 4 years of CO2 injection plus 4 years of post-injection monitoring – Startup scheduled for 4th Quarter 2010 • Southern Co. is leading the project and will install and operate the plant; MHI is designing the CO2 capture facility • EPRI will measure and report CO2 capture performance, operability, and reliability • EPRI is managing CO2 injection and monitoring operations under U.S. DOE research partnership © 2009 Electric Power Research Institute, Inc. All rights reserved. 18
  • 19. Questions? Together…Shaping the Future of Electricity Jeffrey Phillips [email protected] Jong Kim [email protected] © 2009 Electric Power Research Institute, Inc. All rights reserved. 19